Organic acid producing microorganism and process for preparing organic acids employing the same

ABSTRACT

A novel microorganism capable of producing organic acids, Mannheimia sp. 55E, and a process for producing organic acid through anaerobic and aerobic incubation using the novel microorganism are provided. The method of producing an organic acid using the microorganism involves incubating Mannheimia sp. 55E with Accession Number KCTC 0769BP in a medium under anaerobic or aerobic conditions and obtaining an organic acid from the medium. Mannheimia sp. 55E produces succinic acid, lactic acid, and formic acid under anaerobic conditions saturated with CO 2 , and succinic acid, lactic acid, acetic acid, and formic acid under aerobic or N 2  anaerobic conditions. Mannheimia sp. 55E is a facultative anaerobe tolerant of oxygen. Thus, the use of Mannheimia sp. 55E in producing organic acids can eliminate a problem of process instability, which would occur by the presence of oxygen in a fermentation process of producing organic acids using an obligate anaerobic microorganism.

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The present invention relates to a microorganism capable of producing organic acids and a process for producing organic acids using the microorganism, and more particularly, to a new microorganism, Mannheimia sp. 55E, capable of producing organic acids and a process for producing organic acids through incubation of the microorganism in anaerobic or aerobic conditions.

[0003] 2. Description of the Related Art

[0004] Thanks to the progress of the petrochemical industry, most chemical substances have been produced from petroleum and natural gases. However, restrictions on the production of chemical substances is becoming more rigid worldwide with the recent rise of environmental concerns such as global warming, thereby increasing the need for the development of an alternate to the conventional process of producing chemicals.

[0005] The rapid advance of microorganism cultivation and genetic engineering technology has placed biochemical productions of chemical substances at a competitive position to the conventional petrochemical process. Biochemical methods are known to be environmentally compatible, thus being capable of solving environmental problems, because they can suppress generation of gases that cause global warming, such as carbon dioxide (CO₂), with use of inexpensive renewable resources. Therefore, approaches to cost reduction through isolation of new strains and process improvement are getting spread in the biochemical field. In addition, increased market values of biochemical materials have boosted research into the production of the biochemical materials from biomass using microorganisms throughout the world.

[0006] In particular, focus on biochemical materials, particularly succinic acid and lactic acid, is increasing due to their cost competitiveness and wide applications as biodegradable plastic monomers, food additives, and intermediate products of other organic compounds.

[0007] A study on the biological production of succinic acid was started in 1938 by Lockwood who reported production of succinic acid from sugar using Fusarium martii with a 18% yield. It was reported that production of succinic acid through glycolysis of a variety of anaerobic microorganisms such as Succinivibrio dextrinosolvens, Fibrobacter succinogenes, and Ruminococcus flavefaciens (Zeikus, Annu, Rev. Microbiol., 34:423-464, 1980). Any microorganism capable of producing succinic acid with high yield for industrial use, except for Anaerobiospirillum succiniciproducens known to be able to produce succinic acid from glucose with high yield and concentration in the presence of excess carbon, was not disclosed (David et al., Int J. Syst. Bacteriol., 26:498-504, 1976). Because Anerobiospirillum succiniciproducens is an obligate anaerobic microorganism, stable fermentation using the microorganism for production of the succinic acid is not ensured even with the presence of trace oxygen.

[0008] A variety of factors, such as production yield, fermentation conditions, etc., should be carefully considered for economical production of organic acids through microorganism fermentation. In particular, isolation of new microorganisms capable of producing organic acids has priority over the other factors to consider. Most microorganisms currently available to produce organic acids are anaerobic microorganisms, so costly cultivation equipment is required, and it is very likely that intended fermentation fails due to the presence of trace oxygen. Therefore, there is an urgent need for development of microorganisms having a tolerance to oxygen and capable of producing organic acids with high yield.

[0009] As a result of research on such oxygen-tolerant microorganisms being able to produce organic acids with high throughput, the present inventors have succeeded in separating a new facultative anaerobe, Mannheimia sp. 55E, from the bovine rumen fluid, and identifying the new microorganism to be tolerant of oxygen and able to produce organic acids in anaerobic and aerobic conditions.

SUMMARY OF THE INVENTION

[0010] It is a first object of the present invention to provide a new microorganism, Mannheimia sp. 55E (KCTC 0769BP), capable of producing organic acids.

[0011] It is a second object of the present invention to provide a process for producing organic acids under anaerobic and aerobic conditions using the microorganism.

[0012] To isolate a new microorganism tolerant of oxygen and capable of producing organic acids with high yield, the present inventors inoculated dilute samples from the rumen fluid on a solid medium to give rise to individual colonies and incubated on a growth medium containing excess carbon dioxide (CO₂) to screen strains having the ability to produce succinic acid. The screened strain was subjected to 6S rDNA analysis to determine whether they have similarity to previously known strains. As a result, the isolated strain was identified as a new microorganism with a 95% similarity to Mannheimia varigena and designated as Mannheimia sp. 55E. A deposit of Mannheimia sp. 55E was made Apr. 10, 2000 to the Korean Collection for Type Cultures (KCTC), an International Depository Authority (IDA) in Korea Research Institute of Bioscience and Biotechnology (KRIBB) (52 Oun-dong, Yusong-gu, Taejon, Republic of Korea) and was given Accession Number KCTC 0769BP.

[0013] Mannheimia sp. 55E identified in the present invention is facultative anaerobic, gram-negative, non-motile, appears as rods or coccobacilli, does not form endospores, and has the ability to produce organic acids such as succinic acid, lactic acid, acetic acid, formic acid, etc. Mannheimia sp. 55E has a growth temperature range of 30-50° C. with an optimal growth temperature of 39° C. and a pH range of 6.0-7.5 with an optimal pH of 6.5.

[0014] A process for producing organic acids using Mannheimia sp. 55E involves incubating Mannheimia sp. 55E (KCTC 0769BP) under anaerobic or aerobic conditions and obtaining organic acids therefrom. The anaerobic conditions are created with a supply of carbon dioxide (CO₂) or nitrogen at a flow rate of 0.1-0.4 vvm, preferably 0.2-0.3 vvm, and most preferably 2.25 vvm. The aerobic conditions are created with a supply of oxygen (O₂) at a flow rate of 0.5-1.0 vvm, preferably 0.7-0.8 vvm, and most preferably 0.75 vvm.

[0015] Any medium is available for the culture of Mannheimia sp. 55E without limitations, but preferably the content of glucose in a medium is in the range of 5-60 g/L, and most preferably 20 g/L. The incubation is carried out at a temperature of 35-45° C., preferably at a temperature of 38-41° C., and most preferably at 39° C., and at pH 6.0-7.5, preferably at pH 6.3-6.7, and most preferably at pH 6.5.

[0016] Lactic acid, citric acid, succinic acid, or formic acid is produced under the anaerobic conditions. It is preferable to produce the anaerobic conditions using CO₂ for higher yield of succinic acid and N₂ for higher yield of lactic acid. Lactic acid, citric acid, or formic acid is produced under the aerobic conditions with the lactic acid having the highest yield.

BRIEF DESCRIPTION OF THE DRAWINGS

[0017] The above and other features and advantages of the present invention will become more apparent by describing in detail exemplary embodiments thereof with reference to the attached drawings in which:

[0018]FIG. 1 is a phylogenetic tree constructed by 16S RNA analysis for Mannheimia sp. 55E;

[0019]FIG. 2 is a scanning electron microscope (SEM) photo showing the morphological characteristics of Mannheimia sp. 55E;

[0020]FIG. 3 is a graph showing the fermentation characteristics of Mannheimia sp. 55E under anaerobic conditions saturated with CO₂;

[0021]FIG. 4 is a graph showing the fermentation characteristics of Mannheimia sp. 55E under anaerobic conditions saturated with N₂; and

[0022]FIG. 5 is a graph showing the fermentation characteristics of Mannheimia sp. 55E under aerobic conditions.

DETAILED DESCRIPTION OF THE INVENTION

[0023] The present invention will be described in greater detail by means of the following examples. The following examples are for illustrative purposes and are not intended to limit the scope of the invention.

EXAMPLE 1 Isolation and Identification of Mannheimia sp. 55E by 16S rDNA Sequence Analysis

[0024] 1 ml of the bovine rumen fluid was subjected to 100 fold dilution with a medium consisting of 20 g of glucose, 5 g of polypeptone, 5 g of yeast extract, 3 g of K₂HPO₄, 1 g of NaCl, 5 g of (NH₄)₂SO₄, 0.2 g of CaCl₂.2H₂O, 0.2 g of MaCl₂.6H₂O, and 5 g of Na₂CO₃ per liter, followed by plating on a 1%-agarose solid medium having the same composition as the medium above and incubation for 10 hours. Individual colonies were isolated from the cultures and transferred to and incubated in 3 ml of the above medium saturated with CO₂ for 10 hours. The yield of succinic acid in the medium was measured by high performance liquid chromatography (HPLC, Aminex HPX-87H column, Bio-Rad, U.S.A.), and a strain producing succinic acid with a 50% or greater yield was screened. As a result of a physiological property assessment on the screened strain, the screened strain was found to be gram negative and non-endospore forming. The strain growth was observed at a temperature of 30-50° C. with the optimal growth temperature of 39° C., and at a pH of 6.0-7.5 with the optimal growth pH of 6.5.

[0025] Genomic DNA was isolated from the screened strain by applying the Rochelle's method (Rochelle et al., FEMS Microbiol., Lett., 100:59-66, 1992). Polymerase chain reaction (PCR) was carried out using the isolated genomic DNA as a template, primer 1 (5′-AGAGTTTGATCMTGGCTCAG-3′ (SEQ ID NO. 1)), and primer 2 (5′-AAGGAGGTGWTCCARCC-3′ (SEQ ID NO. 2)) to amplify 16S rDNA. The sequence of the amplified products of 16S rDNA was identified, and the similarity of the 16S rDNA to other known strains was analyzed using a DNA sequence analysis program, PHYLIP (PHYlogeny Inference Package, version 3.5c). Table 1 shows the result of the similarity analysis for species, and FIG. 1 is a phylogenetic tree constructed through the similarity analysis.

[0026] As shown in Table 1 and FIG. 1, the isolated strain is proved to be a new strain that belongs to the Mannheimia genus in the Pasteurellaceae family with a 95.1% similarity to Mannheimia variaena, and designated Mannheimia sp. 55E. A deposit of Mannheimia sp. 55E was made Apr. 10, 2000 to the Korean Collection for Type Cultures (KCTC), an International Depository Authority (IDA) in Korea Research Institute of Bioscience and Biotechnology (KRIBB) (52 Oun-dong, Yusong-gu, Taejon, Republic of Korea) and was given Accession Number KCTC 0769BP. TABLE 1 Results of 16S r DNA Analysis for Similarity Species Code No. Similarity Mannheimia varigena (CCUG 38462T) AF053893 95.1 Mannheimia granulomatis (ATCC 49244T) AF053902 94.9 Mannheimia ruminalis (CCUG 38470T) AF053900 94.7 Mannheimia glucosida (CCUG 38457T) AF053889 94.7 Pasteurella trehalosi (NCTC 11550) U57073 94.7 Pasteurella dagmatis (ATCC 43325T) M75051 94.3 Mannheimia haemolytica (NCTC 9380T) AF060699 94.1 Pasteurella avium (NCTC 11297T) M75058 94.0 Pateurella aerogenes (ATCC 27883T) M75048 94.0 Pasteurella bettyae (CCUG 2042T) L06088 94.0 Pasteurella volantium (NCTC 3438T) M75070 93.8 Pasteurella mairii (CCUG 27189T) AF024532 93.8 Pasteurella multocida (NCTC 10322T) M35018 93.8 Pasteurella langaaensis (ATCC 43328T) M75053 93.7 Pasteurella gallinarum (NCTC 11188T) M75059 93.5 Pasteurella stomatis (ATCC 43327T) M75050 93.2 Pasteurella canis (ATCC 43326T) M75049 93.1 Haemophilus influenzae T M35019 92.5 Pasteurella pneumotropica (NCTC 8141T) M75083 92.3 Pasteurella anatis (ATCC 43329T) M75054 92.0 Pasteurella testudinis (CCUG 19802T) L06090 91.3 Vibrio cholerae (ATCC 14035T) Z21856 87.8 E. coli J01695 86.6

EXAMPLE 2 Characteristics of Mannheimia sp. 55E

[0027] Mannheimia sp. 55E was cultured on a blood agar plate, which is known to be suitable for the growth of Mannheimia species, at 39° C. for 24 hours. As a result, colonies having a diameter of 1-2 mm with smooth greyish surface were observed. Single cells of Mannheimia sp. 55E were observed using a scanning electron microscope (SEM). As shown in FIG. 2, cells of Mannheimia sp. 55E appear as rods or coccobaccilli having dimensions 0.3-0.5 by 1.0 microns.

EXAMPLE 3 Fermentation Characteristics of Mannheimia sp. 55E Under Anaerobic Conditions Saturated with CO₂

[0028] To investigate fermentation power of Mannheimia sp. 55E, it was incubated under anaerobic conditions saturated with CO₂, and the reaction products were analyzed.

[0029] 100 ml of a pre-culture medium consisting of 20 g of glucose, 5 g of polypeptone, 5 g of yeast extract, 3 g of K₂HPO₄, 1 g of NaCl, 1 g of (NH₄)₂SO₄, 0.2 g of CaCl₂.2H₂O, 0.2 g of MaCl₂.6H₂O, and 10 g of MgCO₃ per liter was prepared, and CO₂ gas was supplied to the medium. Inoculation of Mannheimia sp. 55E was followed by pre-culture at 39° C. for 9 hours.

[0030] 0.9 ml of a main culture medium consisting of 20 g of glucose, 5 g of polypeptone, 5 g of yeast extract, 3 g of K₂HPO₄, 1 g of NaCl, 1 g of (NH₄)₂SO₄, 0.2 g of CaCl₂.2H₂O, 0.2 g of MaCl₂.6H₂O, and 10 g of MgCO₃ per liter was placed inside a 2.5L incubator. 100 ml of the pre-culture of succinic acid producing microorganism was transferred to the main culture medium, followed by fed-batch culture at 39° C. at pH 6.5 with supply of CO₂ gas at a flow rate of 0.25 vvm. Culture media were sampled at 1-hour intervals during the incubation and cell concentration, and the amounts of succinic acid, glucose, acetic acid, and formic acid were measured by a spectrophotometer (Ultraspec 3000, Pharmacia Biotech., Sweden).

[0031]FIG. 3 is a graph showing variations in concentration of cells (), succinic acid (◯), glucose (), lactic acid (⋄), and formic acid (□) with respect to incubation time. As shown in FIG. 3, after a 7.5-hour incubation, 19.8 g/L of glucose is consumed, and 13.3 g/L lactic acid is produced with a yield of 67% (amount of produced succinic acid per amount of consumed glucose). Volumetric productivity for succinic acid (amount of produced succinic acid per hour) is 1.8 g/L/h.

[0032] The method of producing succinic acid using Mannheimia sp. 55E under anaerobic conditions saturated with CO₂ has a slightly lower yield, but about 80% greater volumetric productivity than a conventional anaerobic method of producing succinic acid using Anaerobiospirillum succiniciproducens (ATCC 29305) (Lee et al., Enzyme Microbiol. Technol., 24:549-554, 1999).

EXAMPLE 4 Fermentation Characteristics of Mannheimia sp. 55E Under Anaerobic Conditions Saturated with N₂

[0033] To investigate fermentation power of Mannheimia sp. 55E under anaerobic conditions saturated with N₂, incubation was carried out for 22 hours in the same manner as in Example 3, except that nitrogen was supplied at a flow rate of 0.25 vvm. Culture media were sampled at 1-hour intervals during the incubation, and cell concentration and the amounts of lactic acid, glucose, formic acid, acetic acid, and succinic acid were measured by the same method as in Example 3.

[0034]FIG. 4 is a graph showing variations in concentration of cells (), succinic acid (◯), lactic acid (⋄), glucose (▪), formic acid (□), and acetic acid (Δ) with respect to incubation time. Unlike the result of FIG. 3, as shown in FIG. 4, Mannheimia sp. 55E according to the present invention produces lactic acid as a major product and succinic acid with a low yield less than 9% under anaerobic conditions saturated with N₂. During the anaerobic fermentation, 18 g/L of glucose is consumed, and 9.8 g/L lactic acid is produced with a yield of 54% and a volumetric productivity of 0.45 g/L/h.

[0035] This result indicates that Mannheimia sp. 55E needs CO₂ to produce succinic acid. Mannheimia sp. 55E is considered as fixing CO₂ to use it in the production of succinic acid.

EXAMPLE 5 Fermentation Characteristics of Mannheimia sp. 55E Under Aerobic Conditions Saturated with O₂

[0036] To investigate fermentation power of Mannheimia sp. 55E under aerobic conditions, incubation was carried out for 14 hours in the same manner as in Example 3, except that oxygen was supplied at a flow rate of 0.75 vvm. Culture media were sampled at 1-hour intervals during the incubation, and cell concentration and the amounts of lactic acid, glucose, and acetic acid were measured by the same method as in Example 3.

[0037]FIG. 5 is a graph showing variations in concentration of cells (), lactic acid (⋄), glucose (▪), and acetic acid (Δ) with respect to incubation time. As shown in FIG. 5, Mannheimia sp. 55E according to the present invention shows an increase in cell concentration up to 11 by optical density (OD) at 660 nm after fermentation under O₂ aerobic conditions. This result indicates that Mannheimia sp. 55E is a facultative anaerobe whose cell growth is unaffected by the presence of oxygen. This aerobic fermentation using Mannheimia sp. 55E does not produce succinic acid and formic acid at all and produces lactic acid as a major product. During the aerobic fermentation, 22 g/L of glucose is consumed, and 9.8 g/L lactic acid is produced with a yield of 45% and a volumetric productivity of 0.7 g/L/h.

[0038] As supported by the results described above, since Mannheimia sp. 55E according to the present invention is a facultative anaerobe, removal of dissolved oxygen is unnecessary for the production of succinic acid under CO₂ anaerobic conditions. It is expected that the production of succinic acid be unaffected by the presence of oxygen, as long as the amount of CO₂ supplied for the fermentation is sufficient enough.

[0039] The present invention provides Mannheimia sp. 55E, a novel microorganism capable of producing organic acids, and a process for producing organic acid through anaerobic and aerobic fermentation using the novel microorganism. As described above, Mannheimia sp. 55E according to the present invention produces succinic acid, lactic acid, and formic acid under CO₂ anaerobic conditions, and succinic acid, lactic acid, acetic acid, and formic acid under aerobic or N₂ anaerobic conditions. Mannheimia sp. 55E according to the present invention is a facultative anaerobe tolerant of oxygen. Thus, the use of Mannheimia sp. 55E in producing organic acids can eliminate a problem of process instability, which would occur by the presence of oxygen in the conventional fermentation process of producing organic acids using an obligate anaerobic microorganism.

[0040] While this invention has been particularly shown and described with reference to preferred embodiments thereof, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.

1 2 1 20 DNA Artificial Sequence primer 1 agagtttgat cmtggctcag 20 2 17 DNA Artificial Sequence primer 2 aaggaggtgw tccarcc 17 

What is claimed is:
 1. Mannheimia sp. 55E with Accession Number KCTC 0769BP, capable of producing an organic acid under anaerobic and aerobic conditions.
 2. A process for producing an organic acid, the process comprising: incubating Mannheimia sp. 55E with Accession Number KCTC 0769BP of claim 1 in a medium containing 5-60 g/L of glucose under anaerobic conditions saturated with carbon dioxide or nitrogen; and obtaining an organic acid from the medium.
 3. The process of claim 2, wherein the organic acid is one of succinic acid, formic acid, acetic acid, and lactic acid.
 4. The process of claim 2, wherein the incubation is carried out at a temperature of 35-45° C. at a pH of 6.0-7.5 with a supply of carbon dioxide or nitrogen at a flow rate of 0.1-0.4 vvm.
 5. A process for producing succinic acid, the process comprising: incubating Mannheimia sp. 55E with Accession Number KCTC 0769BP of claim 1 in a medium containing 5-60 g/L of glucose at a temperature of 35-45° C. at a pH of 6.0-7.5 with a supply of carbon dioxide at a flow rate of 0.1-0.4 vvm; and obtaining succinic acid from the medium.
 6. A process for producing lactic acid, the process comprising: incubating Mannheimia sp. 55E with Accession Number KCTC 0769BP of claim 1 in a medium containing 5-60 g/L of glucose at a temperature of 35-45° C. at a pH of 6.0-7.5 with a supply of nitrogen at a flow rate of 0.1-0.4 vvm; and obtaining lactic acid from the medium.
 7. A process for producing an organic acid, the process comprising: incubating Mannheimia sp. 55E with Accession Number KCTC 0769BP of claim 1 in a medium containing 5-60 g/L of glucose under aerobic conditions; and obtaining an organic acid from the medium.
 8. The process of claim 7, wherein the organic acid is one of lactic acid and acetic acid.
 9. The process of claim 7, wherein the incubation is carried out at a temperature of 35-45° C. at a pH of 6.0-7.5 with a supply of oxygen at a flow rate of 0.5-1.0 vvm.
 10. A process for producing lactic acid, the process comprising: incubating Mannheimia sp. 55E with Accession Number KCTC 0769BP of claim 1 in a medium containing 5-60 g/L of glucose at a temperature of 35-45° C. at a pH of 6.0-7.5 with a supply of oxygen at a flow rate of 0.5-1.0 vvm; and obtaining lactic acid from the medium. 